US4150099A - Synthetic halloysites - Google Patents

Synthetic halloysites Download PDF

Info

Publication number
US4150099A
US4150099A US05/525,205 US52520574A US4150099A US 4150099 A US4150099 A US 4150099A US 52520574 A US52520574 A US 52520574A US 4150099 A US4150099 A US 4150099A
Authority
US
United States
Prior art keywords
halloysite
sub
synthetic
sio
halloysites
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US05/525,205
Inventor
Harry E. Robson
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ExxonMobil Technology and Engineering Co
Original Assignee
Exxon Research and Engineering Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Exxon Research and Engineering Co filed Critical Exxon Research and Engineering Co
Priority to US05/525,205 priority Critical patent/US4150099A/en
Priority to US05/740,868 priority patent/US4098676A/en
Application granted granted Critical
Publication of US4150099A publication Critical patent/US4150099A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/02—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils characterised by the catalyst used
    • C10G11/04—Oxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/16—Clays or other mineral silicates
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B33/00—Silicon; Compounds thereof
    • C01B33/20—Silicates
    • C01B33/26—Aluminium-containing silicates, i.e. silico-aluminates
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • C07C4/08—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by splitting-off an aliphatic or cycloaliphatic part from the molecule
    • C07C4/12—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by splitting-off an aliphatic or cycloaliphatic part from the molecule from hydrocarbons containing a six-membered aromatic ring, e.g. propyltoluene to vinyltoluene
    • C07C4/14—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by splitting-off an aliphatic or cycloaliphatic part from the molecule from hydrocarbons containing a six-membered aromatic ring, e.g. propyltoluene to vinyltoluene splitting taking place at an aromatic-aliphatic bond
    • C07C4/18—Catalytic processes
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
    • C10G49/02—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
    • C07C2521/12—Silica and alumina

Definitions

  • This invention relates to a novel composition of matter useful as a catalyst and/or catalyst base in hydrocarbon conversion reactions. More particularly, this invention relates to synthetic halloysite, its preparation and its use in hydrocarbon conversion reactions such as cracking, hydrocracking, hydrofining, desulfurization, and demetallization.
  • Halloysite is a well-known kaolin clay mineral having the empirical formula Al 2 O 3 :2SiO 2 :2H 2 O.
  • a complete chemical analysis for halloysite is given in the "Encyclopedia of Chemical Technology," 2nd Edition, Vol. 5, page 545 (Interscience Publishers). Further descriptions concerning the properties and characteristics of naturally-occurring halloysite may be found in the literature such as, for example, Thomas F. Bates et al. (1950), Morphology and Structure of Endellite and Halloysite, The American Mineralogist, Vol. 35, pages 463-484; Thomas F.
  • Natural halloysite has been used heretofore in the petroleum art as a catalytic cracking catalyst.
  • naturally-occurring halloysite contains various metals, such as iron, which are detrimental to its effectiveness as a hydrocarbon conversion catalyst. It has been found, therefore, necessary to subject the naturally occurring halloysite to acid treatment in order to reduce the iron content and thereby increase its effectiveness as a hydrocarbon conversion catalyst.
  • acid treatment often does substantial damage to the crystalline structure of the halloysite which drastically limits its use as a catalyst in hydrocarbon conversion processes.
  • a synthetic halloysite which is substantially iron-free is obtained by crystallization from a reaction mixture containing hydrous alumina gel and aqueous silica sol.
  • metal substituted synthetic halloysites are prepared by coprecipitation of metal hydroxides with the alumina gel.
  • the halloysite of the invention is prepared by crystallization from an aqueous mixture containing a mixture of alumina gel and a silica source maintained at a pH of 4 to 10 for at least about 16 hours at a temperature in excess of 200° C.
  • a preferred reaction scheme is given by the following equations:
  • metal substituted synthetic halloysites can be prepared in accordance with the invention by coprecipitation of a hydroxide of the metal with the alumina gel.
  • the empirical formula for such metal substituted synthetic halloysites which may have an SiO 2 /Al 2 O 3 ratio greater than the stoichiometric amount, can be expressed by the following formula:
  • M is a metal selected from Groups IIA, IIIB, VIB and VIII of the Periodic Table
  • n valence of M
  • x 0 to 1, preferably 0.8 to 1.0
  • Preparation of the synthetic halloysite of the Invention involves the reaction of hydrous alumina gel, i.e., Al(OH) 3 , and a source of silica.
  • the hydrous alumina gel is prepared in accordance with known techniques such as by the reaction of aqueous mixtures of aluminum chloride or aluminum sulfate and an inorganic base such as NH 4 OH, NaOH or NaAlO 2 , and the like.
  • Preparation of alumina gel by use of ammonium hydroxide is preferable to the use of sodium hydroxide since it is desirable to maintain the soda (Na 2 O) content to a low level and because the more alkaline gels tend to form crystalline boehmite.
  • the silica source may include those sources which are conventionally used for the preparation of crystalline aluminosilicate zeolites. These include silicic acid, silica sol, silica gel, sodium silicate, etc. Silica sols are particularly useful. These are colloidal dispersions of discrete spherical particles of surface-hydroxylated silica such as is sold by E. I. du Pont de Nemours & Company, Inc. under the trademark "Ludox.”
  • the proportions of the reactants employed in the initial reaction mixture are determined from the following molar ratio of reactants.
  • the pH of the reaction mixture should be adjusted to a range of about 4 to 10, preferably 6 to 8.
  • the temperature of the reaction mixture should preferably be maintained at between about 230° and 270° C., more preferably 240° to 250° C., for a period from about 2 hours to 100 hours or more.
  • the time necessary for crystallization will depend, of course, upon the temperature of the reaction mixture.
  • the crystallization of the synthetic halloysite occurs in about 24 hours at a temperature of about 250° C.
  • the catalytic activity of the synthetic halloysites of the invention can be improved by incorporating therein metals selected from Groups IIA, IIIB, VIB, and VIII of the Periodic Table as given in "Websters Seventh New Collegiate Dictionary," (1963) published by G. C. Merriam Company.
  • metals selected from Groups IIA, IIIB, VIB, and VIII of the Periodic Table as given in "Websters Seventh New Collegiate Dictionary," (1963) published by G. C. Merriam Company.
  • Specific examples of such metals include, among others, magnesium, lanthanum, molybdenum, cobalt, nickel, palladium, platinum and rare earths.
  • Particularly preferred metals include magnesium, nickel, cobalt and lanthanum.
  • the metals are incorporated into the synthetic halloysite structure by adding soluble salts of the metal to the reaction mixture or by coprecipitation of the metal hydroxide with Al(OH) 3 .
  • the metals are most conveniently added to the reaction mixture in the form of their hydroxides.
  • the synthetic halloysite of the invention particularly when substituted with the afore-described metals, is useful for catalytic cracking, hydrocracking, desulfurization, demetallization and other hydrocarbon conversion processes.
  • substituted halloysites of the invention containing metals such as magnesium, lanthanum and rare earths such as cerium, praseodymium, neodymium, gadolinium, etc., are useful in catalytic cracking of petroleum feedstocks.
  • Synthetic halloysite containing nickel, cobalt, palladium, platinum, and the like are particularly useful for hydrocracking petroleum feedstocks.
  • feedstocks suitable for conversion in accordance with the invention include any of the well-known feeds conventionally employed in hydrocarbon conversion processes. Usually they will be petroleum derived, although other sources such as shale oil are not to be excluded. Typical of such feeds are heavy and light virgin gas oils, heavy and light virgin naphthas, solvent extracted gas oils, coker gas oils, steam-cracked gas oils, middle distillates, steam-cracked naphthas, coker naphthas, cycle oils, deasphalted residua, etc.
  • the halloysite structure of the composition of this invention has been confirmed by X-ray diffraction and electron microscopy.
  • the synthetic halloysites of the invention have surface areas ranging from about 85 sq. meters/gram to about 200 sq. meters/gram (BET Method as used, for example, in U.S. Pat. No. 3,804,741) as compared to naturally occurring halloysite which has a surface area generally within the range of 40-85 sq. meters/gram (BET Method).
  • the synthetic halloysite of the invention will be substantially iron-free, i.e., less than 0.05% iron, as compared to naturally occurring halloysite which contains significant amounts of iron.
  • the synthetic and naturally occurring halloysites also differ in that the physical form of the synthetic halloysite is flakes, while the physical form of the natural halloysite has a tube-like configuration.
  • the synthetic halloysite has considerably better catalytic activity than natural halloysite under analogous hydrocarbon conversion conditions.
  • the synthetic halloysite has the same empirical formula as naturally occurring halloysite, the higher surface area, the elimination of iron and the presence of selective metals makes the synthetic halloysite a more effective hydrocarbon conversion catalyst.
  • This example illustrates a general procedure for the preparation of the synthetic halloysite of the invention.
  • a solution consisting of 962 grams of AlCl 3 .6H 2 O in 3,200 cubic centimeters (cc) of water were added to a 1 gallon stainless steel vessel.
  • the solution was stirred at ambient conditions and neutralized with about 740 cc. of a 28% ammonia solution, thereby producing a pH greater than 8.
  • the Al(OH) 3 gel produced was washed with water until it was substantially chloride-free.
  • the blend of silica sol and alumina gel was then transferred to a 200 cc. Monel autoclave where it was heated at 246° C. for 48 hours to produce synthetic halloysite.
  • Example 2 Using the general procedure of Example 1, a number of synthetic halloysites were prepared to determine the surface area of synthetic halloysite prepared in accordance with the invention. The results given below in Table I show that the surface area expressed in square meters per gram is higher than naturally occurring halloysite.
  • Example 2 Using the general preparation procedure given in Example 1, a number of metal-substituted synthetic halloysites were prepared by precipitating insoluble hydroxides of various metals with aluminum hydroxide and blending the resultant washed gel with the silica sol. The reaction conditions and the amount of substituted metal in the synthetic halloysite product are given in Table II.
  • the catalysts prepared in the previous example were pressed on a hydraulic ram, the compacted forms of the catalyst then crushed to 14-35 mesh (Tyler series), and then calcined at 540° C. for 16 hours. Portions of this granular catalyst were charged to reactors and the temperature adjusted to 280° C. A stream of helium was passed through a saturator filled with cumene at 18° C. and passed into the reactor and contacted with the catalyst. The effluent from the reactor was analyzed by gas chromatography to determine the amount of conversion of the cumene to benzene and propylene. The results obtained were compared with natural halloysite (API Standard No. 13). The results obtained were given below in Table III.
  • the radiation source was the K-alpha doublet for copper.
  • a Geiger counter spectrometer with a strip chart pen recorder was used in recording the data.
  • the peak heights I, and the positions as a function of 2 ⁇ , where ⁇ is the Bragg angle, were read from the spectrometer chart. From these, the relative intensities I were observed.
  • the interplanar spacing, d, in Angstrom units, corresponding to the recorded lines were determined by reference to standard tables.
  • the more significant interplanar spacings, i.e., d values, for a typical synthetic halloysite of the invention, natural halloysite and kaolinite are shown below in Table IV.
  • the synthetic halloysite of the invention the relative intensities of the lines are expressed as s. (strong), m. (medium) and w. (weak).
  • the d line at 4.43 A is significant.
  • Kaolinite has d lines at 4.48 A and 4.37 A, but no strong intensity d line at 4.43 A as in the case of the synthetic halloysite of the invention.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Materials Engineering (AREA)
  • Silicates, Zeolites, And Molecular Sieves (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

A synthetic halloysite which is substantially iron-free is obtained by crystallization from a reaction mixture containing hydrous alumina gel and aqueous silica sol. Metal substituted synthetic halloysites can be prepared by coprecipitation of metal hydroxides with the alumina gel.

Description

BACKGROUND OF THE INVENTION
1. Field of the Invention
This invention relates to a novel composition of matter useful as a catalyst and/or catalyst base in hydrocarbon conversion reactions. More particularly, this invention relates to synthetic halloysite, its preparation and its use in hydrocarbon conversion reactions such as cracking, hydrocracking, hydrofining, desulfurization, and demetallization.
2. Description of the Prior Art
Halloysite is a well-known kaolin clay mineral having the empirical formula Al2 O3 :2SiO2 :2H2 O. A complete chemical analysis for halloysite is given in the "Encyclopedia of Chemical Technology," 2nd Edition, Vol. 5, page 545 (Interscience Publishers). Further descriptions concerning the properties and characteristics of naturally-occurring halloysite may be found in the literature such as, for example, Thomas F. Bates et al. (1950), Morphology and Structure of Endellite and Halloysite, The American Mineralogist, Vol. 35, pages 463-484; Thomas F. Bates et al., Further Observations on the Morphology of Chrysotile and Halloysite, Proceedings National Conference on Clays and Clay Minerals, VI, Berkeley, 1957 pages 237-248; and G. Brown, The X-Ray Identification and Crystal Structures of Clay Minerals, Mineralogical Society (Clay Minerals Group), London, 1961, pages 68-77.
Natural halloysite has been used heretofore in the petroleum art as a catalytic cracking catalyst. Unfortunately, naturally-occurring halloysite contains various metals, such as iron, which are detrimental to its effectiveness as a hydrocarbon conversion catalyst. It has been found, therefore, necessary to subject the naturally occurring halloysite to acid treatment in order to reduce the iron content and thereby increase its effectiveness as a hydrocarbon conversion catalyst. Unfortunately, acid treatment often does substantial damage to the crystalline structure of the halloysite which drastically limits its use as a catalyst in hydrocarbon conversion processes.
SUMMARY OF THE INVENTION
In accordance with the present invention, a synthetic halloysite which is substantially iron-free is obtained by crystallization from a reaction mixture containing hydrous alumina gel and aqueous silica sol. In a further embodiment of the invention, metal substituted synthetic halloysites are prepared by coprecipitation of metal hydroxides with the alumina gel.
In general, the halloysite of the invention is prepared by crystallization from an aqueous mixture containing a mixture of alumina gel and a silica source maintained at a pH of 4 to 10 for at least about 16 hours at a temperature in excess of 200° C. A preferred reaction scheme is given by the following equations:
AlCl.sub.3 (aqueous solution)+NH.sub.4 OH→Al(OH).sub.3.50 H.sub.2 O (gel)+NH.sub.4 Cl (solution)
2 Al (OH).sub.3.50 H.sub.2 O (washed gel)+2 SiO.sub.2.8 H.sub.2 O (sol) ∵Al.sub.2 (OH).sub.4 Si.sub.2 O.sub.5 (synthetic halloysite) +117 H.sub.2 O
metal substituted synthetic halloysites can be prepared in accordance with the invention by coprecipitation of a hydroxide of the metal with the alumina gel. The empirical formula for such metal substituted synthetic halloysites, which may have an SiO2 /Al2 O3 ratio greater than the stoichiometric amount, can be expressed by the following formula:
[x Al+(3/n) (1-x)M]2O3.(2+y) SiO.sub.2.2H.sub.2 O
where
M is a metal selected from Groups IIA, IIIB, VIB and VIII of the Periodic Table
n is valence of M
x=0 to 1, preferably 0.8 to 1.0
y=0 to 1.
Preparation of the synthetic halloysite of the Invention involves the reaction of hydrous alumina gel, i.e., Al(OH)3, and a source of silica. The hydrous alumina gel is prepared in accordance with known techniques such as by the reaction of aqueous mixtures of aluminum chloride or aluminum sulfate and an inorganic base such as NH4 OH, NaOH or NaAlO2, and the like. Preparation of alumina gel by use of ammonium hydroxide is preferable to the use of sodium hydroxide since it is desirable to maintain the soda (Na2 O) content to a low level and because the more alkaline gels tend to form crystalline boehmite.
The silica source may include those sources which are conventionally used for the preparation of crystalline aluminosilicate zeolites. These include silicic acid, silica sol, silica gel, sodium silicate, etc. Silica sols are particularly useful. These are colloidal dispersions of discrete spherical particles of surface-hydroxylated silica such as is sold by E. I. du Pont de Nemours & Company, Inc. under the trademark "Ludox."
The proportions of the reactants employed in the initial reaction mixture are determined from the following molar ratio of reactants.
______________________________________                                    
          Reactant Molar Ratio                                            
                              Particularly                                
          General  Preferred  Preferred                                   
______________________________________                                    
Al(OH).sub.3 /SiO.sub.2                                                   
            0.5-1.2    0.8-1.0    0.9-1.0                                 
H.sub.2 O/SiO.sub.2                                                       
            20-60      30-50      40-50                                   
______________________________________
The pH of the reaction mixture should be adjusted to a range of about 4 to 10, preferably 6 to 8. The temperature of the reaction mixture should preferably be maintained at between about 230° and 270° C., more preferably 240° to 250° C., for a period from about 2 hours to 100 hours or more. The time necessary for crystallization will depend, of course, upon the temperature of the reaction mixture. By way of example, the crystallization of the synthetic halloysite occurs in about 24 hours at a temperature of about 250° C.
The catalytic activity of the synthetic halloysites of the invention can be improved by incorporating therein metals selected from Groups IIA, IIIB, VIB, and VIII of the Periodic Table as given in "Websters Seventh New Collegiate Dictionary," (1963) published by G. C. Merriam Company. Specific examples of such metals include, among others, magnesium, lanthanum, molybdenum, cobalt, nickel, palladium, platinum and rare earths. Particularly preferred metals include magnesium, nickel, cobalt and lanthanum. The metals are incorporated into the synthetic halloysite structure by adding soluble salts of the metal to the reaction mixture or by coprecipitation of the metal hydroxide with Al(OH)3. The metals are most conveniently added to the reaction mixture in the form of their hydroxides. The synthetic halloysite of the invention, particularly when substituted with the afore-described metals, is useful for catalytic cracking, hydrocracking, desulfurization, demetallization and other hydrocarbon conversion processes. For example, substituted halloysites of the invention containing metals such as magnesium, lanthanum and rare earths such as cerium, praseodymium, neodymium, gadolinium, etc., are useful in catalytic cracking of petroleum feedstocks. Synthetic halloysite containing nickel, cobalt, palladium, platinum, and the like are particularly useful for hydrocracking petroleum feedstocks.
The feedstocks suitable for conversion in accordance with the invention include any of the well-known feeds conventionally employed in hydrocarbon conversion processes. Usually they will be petroleum derived, although other sources such as shale oil are not to be excluded. Typical of such feeds are heavy and light virgin gas oils, heavy and light virgin naphthas, solvent extracted gas oils, coker gas oils, steam-cracked gas oils, middle distillates, steam-cracked naphthas, coker naphthas, cycle oils, deasphalted residua, etc.
The operating conditions to be employed in the practice of the present invention are well-known and will, of course, vary with the particular conversion reaction desired. The following table summarizes typical reaction conditions effective in the present invention.
__________________________________________________________________________
           Reaction Conditions                                            
Principal            Pressure,                                            
                           Feed Rate                                      
                                 Hydrogen Rate                            
Conversion Desired                                                        
           Temperature, ° F.                                       
                     p.s.i.g.                                             
                           V/V/Hr.                                        
                                 s.c.f./bbl.                              
__________________________________________________________________________
Hydrofining                                                               
           500-800    50-2,000                                            
                           0.1-10.0                                       
                                 500-10,000                               
Hydrocracking                                                             
           450-850   200-2,000                                            
                           0.1-10.0                                       
                                 500-10,000                               
Catalytic Cracking                                                        
           700-1,000 0-50  0.1-20.0                                       
                                 0                                        
Catalytic Reforming                                                       
           850-1,000  50-1,000                                            
                           0.1-20.0                                       
                                 500-10,000                               
__________________________________________________________________________
The halloysite structure of the composition of this invention has been confirmed by X-ray diffraction and electron microscopy. However, there are a number of significant differences between naturally occurring halloysite and the synthetic halloysite of this invention. For example, the synthetic halloysites of the invention have surface areas ranging from about 85 sq. meters/gram to about 200 sq. meters/gram (BET Method as used, for example, in U.S. Pat. No. 3,804,741) as compared to naturally occurring halloysite which has a surface area generally within the range of 40-85 sq. meters/gram (BET Method). Further, the synthetic halloysite of the invention will be substantially iron-free, i.e., less than 0.05% iron, as compared to naturally occurring halloysite which contains significant amounts of iron. The synthetic and naturally occurring halloysites also differ in that the physical form of the synthetic halloysite is flakes, while the physical form of the natural halloysite has a tube-like configuration. Furthermore, it has been discovered that the synthetic halloysite has considerably better catalytic activity than natural halloysite under analogous hydrocarbon conversion conditions. Although the synthetic halloysite has the same empirical formula as naturally occurring halloysite, the higher surface area, the elimination of iron and the presence of selective metals makes the synthetic halloysite a more effective hydrocarbon conversion catalyst.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
The following examples further illustrate the present invention. Unless otherwise specified, all percentages and parts are by weight.
EXAMPLE 1
This example illustrates a general procedure for the preparation of the synthetic halloysite of the invention.
A solution consisting of 962 grams of AlCl3.6H2 O in 3,200 cubic centimeters (cc) of water were added to a 1 gallon stainless steel vessel. The solution was stirred at ambient conditions and neutralized with about 740 cc. of a 28% ammonia solution, thereby producing a pH greater than 8. The Al(OH)3 gel produced was washed with water until it was substantially chloride-free. The washed Al(OH)3 gel was then blended with 790 grams of silica sol sold under the trade name "LS-30 Ludox" by E. I. du Pont de Nemours & Company. The blend of silica sol and alumina gel was then transferred to a 200 cc. Monel autoclave where it was heated at 246° C. for 48 hours to produce synthetic halloysite.
EXAMPLE 2
Using the general procedure of Example 1, a number of synthetic halloysites were prepared to determine the surface area of synthetic halloysite prepared in accordance with the invention. The results given below in Table I show that the surface area expressed in square meters per gram is higher than naturally occurring halloysite.
                                  TABLE I                                 
__________________________________________________________________________
SURFACE AREA OF SYNTHETIC HALLOYSITE                                      
Gel Composition              Crystallization                              
Silica Source                                                             
        Al Source Al/Si                                                   
                      H.sub.2 O/Al.sub.2 O.sub.3                          
                             Conditions                                   
                                       Surface Area.sup.(1)               
                                                (m..sup.2 /g, BET         
__________________________________________________________________________
                                                Method)                   
LS-30 Ludox.sup.(2)                                                       
        Al(OH).sub.3.sup.(3)                                              
                  1.0 72     20 Hr. at 250° C.                     
                                       114                                
LS-30 Ludox                                                               
        Al(OH).sub.3                                                      
                  1.0 89     20 Hr. at 246° C.                     
                                       88                                 
LS-30 Ludox                                                               
        Al(OH).sub.3 +MgCl.sub.2                                          
                  0.9 100    20 Hr. at 246° C.                     
                                       103                                
LS-30 Ludox                                                               
        Al(OH).sub.3 +NiCl.sub.2                                          
                  0.9 100    20 Hr. at 246° C.                     
                                       118                                
LS-30 Ludox                                                               
        Al(OH).sub.3 +FeCl.sub.2                                          
                  0.9 100    20 Hr. at 246° C.                     
                                       91                                 
LS-30 Ludox                                                               
        Al(OH).sub.3 +CoCl.sub.2                                          
                  0.9 100    20 Hr. at 246° C.                     
                                       93                                 
LS-30 Ludox                                                               
        Al(OH).sub.3                                                      
                  1.0 86     48 Hr. at 246° C.                     
                                       99                                 
LS-30 Ludox                                                               
        Al(OH).sub.3 +Mg(OH).sub.2                                        
                  1.0 67     48 Hr. at 255° C.                     
                                       193                                
LS-30 Ludox                                                               
        Al(OH).sub.3 +Mg(OH).sub.2                                        
                  1.0 67     48 Hr. at 246° C.                     
                                       143                                
__________________________________________________________________________
 .sup.(1) Naturally occurring halloysite typically has a surface area in  
 the range of 45-85 m..sup.2 /g.                                          
 .sup.(2) Colloidal silica sol (150 A.) particle size sold by E. I. du Pon
 de Nemours & Company.                                                    
 .sup.(3) AlCl.sub.3 neutralized with NaOH and washed.
EXAMPLE 3
Using the general preparation procedure given in Example 1, a number of metal-substituted synthetic halloysites were prepared by precipitating insoluble hydroxides of various metals with aluminum hydroxide and blending the resultant washed gel with the silica sol. The reaction conditions and the amount of substituted metal in the synthetic halloysite product are given in Table II.
                                  TABLE II                                
__________________________________________________________________________
                          H.sub.2 O/Al.sub.2 O.sub.3                      
                                 Product                                  
                                      Amount of Substituted               
Experiment*                                                               
       Synthesis Gel, Molar Proportions                                   
                          Mole Ratio                                      
                                 Yield**                                  
                                      Metal in Product, Wt.               
__________________________________________________________________________
                                      %                                   
A      SiO.sub.2 Sol + Al(OH).sub.3 + 0.15 Mg(OH).sub.2                   
                          72     81   1.23% Mg                            
B      SiO.sub.2 Sol + Al(OH).sub.3 + 0.15 Ni(OH).sub.2                   
                          66     71   2.6% Ni                             
C      SiO.sub.2 Sol + Al(OH).sub.3 + 0.15 Fe(OH).sub.2                   
                          77     94   4.6% Fe                             
D      SiO.sub.2 Sol + Al(OH).sub.3 + 0.15 Co(OH).sub.2                   
                          84     82   5.6% Co                             
__________________________________________________________________________
 *In all experiments, the Al/Si mole ratio in reaction mixture was 0.94 an
 crystallization conditions were 24 hours at 246° C.               
 **Wt. % of theoretical yield calculated as Al.sub.2                      
 O.sub.3.2SiO.sub.2.2H.sub.2 O.
EXAMPLE 4
The catalysts prepared in the previous example were pressed on a hydraulic ram, the compacted forms of the catalyst then crushed to 14-35 mesh (Tyler series), and then calcined at 540° C. for 16 hours. Portions of this granular catalyst were charged to reactors and the temperature adjusted to 280° C. A stream of helium was passed through a saturator filled with cumene at 18° C. and passed into the reactor and contacted with the catalyst. The effluent from the reactor was analyzed by gas chromatography to determine the amount of conversion of the cumene to benzene and propylene. The results obtained were compared with natural halloysite (API Standard No. 13). The results obtained were given below in Table III.
                                  TABLE III                               
__________________________________________________________________________
CUMENE CRACKING ACTIVITY                                                  
                 W/Hr./W         Cumene Conversion, %                     
Catalyst Description                                                      
                 (G. of Cumene/Hr./G. of Cat.)                            
                                 (At 525° F. After 30              
                                                 K*(Hr..sup.-1)           
__________________________________________________________________________
Natural Halloysite (API #13)                                              
                 0.08             8              0.006                    
Syn. Halloysite of Example 1                                              
                 0.08            16              0.013                    
Mg-Substituted Syn. Halloysite                                            
                 0.075           60              0.068                    
Product A of Example 3                                                    
Ni-Substituted Syn. Halloysite                                            
                 0.081           37              0.038                    
Product B of Example 3                                                    
Fe-Substituted Syn. Halloysite                                            
                 0.22             0              0                        
Product C of Example 3                                                    
Syn. Halloysite of Example 1                                              
                 0.22             5              0.012                    
Co-Substituted Syn. Halloysite                                            
                 0.22            10              0.023                    
Product D of Example 3                                                    
Mg-Substituted Syn. Halloysite                                            
                 0.22            43              0.124                    
Product A of Example 3                                                    
Ni-Substituted Syn. Halloysite                                            
                 0.22            25              0.062                    
Product B of Example 3                                                    
Mg-Substituted Syn. Halloysite                                            
                 0.26            18              0.052                    
Product A of Example 3                                                    
__________________________________________________________________________
 *First order rate constant for cumene cracking reaction.
The above data show the effectiveness of the synthetic halloysites of the invention as cracking catalyst. Synthetic halloysite is more active than natural halloysite and the activity of synthetic halloysite is significantly improved by substituting such metals as magnesium and nickel in the structure. Conversely, the incorporation of iron in synthetic halloysites acts as a catalyst poison, just as it does in natural halloysites.
EXAMPLE 5
This example compares in Table VI the X-ray powder diffraction pattern of a typical synthetic halloysite of the invention with the published patterns for naturally occurring halloysite (ASTM 13-375) and the closely related mineral kaolinite (ASTM 14-164).
In obtaining the X-ray powder diffraction pattern, standard procedures were employed. The radiation source was the K-alpha doublet for copper. A Geiger counter spectrometer with a strip chart pen recorder was used in recording the data. The peak heights I, and the positions as a function of 2θ, where θ is the Bragg angle, were read from the spectrometer chart. From these, the relative intensities I were observed. Also, the interplanar spacing, d, in Angstrom units, corresponding to the recorded lines, were determined by reference to standard tables. The more significant interplanar spacings, i.e., d values, for a typical synthetic halloysite of the invention, natural halloysite and kaolinite are shown below in Table IV. As regards the synthetic halloysite of the invention, the relative intensities of the lines are expressed as s. (strong), m. (medium) and w. (weak).
              TABLE IV                                                    
______________________________________                                    
X-RAY DIFFRACTION PATTERNS FOR HALLOYSITES AND KAOLINITE                  
Synthetic   Natural                                                       
Halloysite* Halloysite**   Kaolinite***                                   
d(A) I     hkl      d(A) I/I.sub.1                                        
                              hkl    d(A)  I/I.sub.1                      
                                                hkl                       
______________________________________                                    
7.3  m.    001      7.4  95   001    7.17   100 001                       
4.43 s.    11,02    4.41  100 11,02  4.48  35   020                       
3.56 m.    002      3.62 65   002    4.37  60   110                       
2.55 m.    20,13    2.58 30   20,13  3.58  80   002                       
2.34 m.    003      2.39,                                                 
                         35   003    2.385 25   003                       
                    2.32                                                  
1.68 m.    24,31    1.70,                                                 
                         20   26,31  1.94  35   132                       
                    1.67                                                  
1.49 m.    33,06                                                          
______________________________________                                    
 *First-listed product of Table I                                         
 **ASTM 13-375                                                            
 ***ASTM 14-164
As regards synthetic halloysite and the related kaolinite mineral, the d line at 4.43 A is significant. Kaolinite has d lines at 4.48 A and 4.37 A, but no strong intensity d line at 4.43 A as in the case of the synthetic halloysite of the invention. The synthetic halloysite of the invention can also be distinguished on the basis that the d line at 4.43 A is of stronger intensity than either the 001 line (d=7.3) or the 002 (d=3.56). Accordingly, the significant X-ray diffraction characteristics of the synthetic halloysite of the invention are as follows:
______________________________________                                    
        d(A)            I                                                 
______________________________________                                    
        7.3±0.2      m                                                 
        4.42±0.02    s                                                 
        3.56±0.04    m                                                 
______________________________________

Claims (5)

What is claimed is:
1. A process for preparing halloysite which comprises forming a reaction mixture of aluminum hydroxide gel, silica sol and water having a Al(OH)3 /SiO2 molar ratio in the range of 0.5 to 1.2 and a H2 O/SiO2 molar ratio in the range of 20 to 60 and maintaining said reaction mixture at a pH in the range of 4 to 10 and a temperature of about between 230° and 270° C. for a time sufficient to permit crystallization of halloysite.
2. The process of claim 1 wherein said aluminum hydroxide gel is prepared from the reaction of hydrous aluminum chloride and ammonia.
3. The process of claim 1 wherein said Al(OH)3 /SiO2 molar ratio is in the range of 0.8 to 1.0 and said H2 O/SiO2 molar ratio is in the range of 30 to 50.
4. The process of claim 3 where said pH is in the range of 6 to 8.
5. The process of claim 4 wherein said Al(OH)3 /SiO2 molar ratio is in the range of 0.9 to 1.0 and said H2 O/SiO2 molar ratio is in the range of 40 to 50.
US05/525,205 1974-11-19 1974-11-19 Synthetic halloysites Expired - Lifetime US4150099A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US05/525,205 US4150099A (en) 1974-11-19 1974-11-19 Synthetic halloysites
US05/740,868 US4098676A (en) 1974-11-19 1976-11-11 Synthetic halloysites as hydrocarbon conversion catalysts

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US05/525,205 US4150099A (en) 1974-11-19 1974-11-19 Synthetic halloysites

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US05/740,868 Division US4098676A (en) 1974-11-19 1976-11-11 Synthetic halloysites as hydrocarbon conversion catalysts

Publications (1)

Publication Number Publication Date
US4150099A true US4150099A (en) 1979-04-17

Family

ID=24092358

Family Applications (2)

Application Number Title Priority Date Filing Date
US05/525,205 Expired - Lifetime US4150099A (en) 1974-11-19 1974-11-19 Synthetic halloysites
US05/740,868 Expired - Lifetime US4098676A (en) 1974-11-19 1976-11-11 Synthetic halloysites as hydrocarbon conversion catalysts

Family Applications After (1)

Application Number Title Priority Date Filing Date
US05/740,868 Expired - Lifetime US4098676A (en) 1974-11-19 1976-11-11 Synthetic halloysites as hydrocarbon conversion catalysts

Country Status (1)

Country Link
US (2) US4150099A (en)

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2465775A1 (en) * 1979-09-26 1981-03-27 Chevron Res CATALYTIC PROCESS FOR HYDROGEN TREATMENT OF A HYDROCARBONATED LOAD
US20050233199A1 (en) * 2004-04-05 2005-10-20 Xingwu Wang Hydrogen storage apparatus comprised of halloysite
US20060076354A1 (en) * 2004-10-07 2006-04-13 Lanzafame John F Hydrogen storage apparatus
US20060166810A1 (en) * 2005-01-25 2006-07-27 Gunderman Robert D Ultracapacitors comprised of mineral microtubules
US20060163752A1 (en) * 2004-04-05 2006-07-27 Xingwu Wang Storage assembly
US20060163160A1 (en) * 2005-01-25 2006-07-27 Weiner Michael L Halloysite microtubule processes, structures, and compositions
US20070106006A1 (en) * 2005-09-02 2007-05-10 Naturalnano, Inc. Polymeric composite including nanoparticle filler
US20080249221A1 (en) * 2007-04-06 2008-10-09 Naturalnano Research, Inc. Polymeric adhesive including nanoparticle filler
US20080248201A1 (en) * 2007-04-06 2008-10-09 Naturalnano Research, Inc. Polymeric coatings including nanoparticle filler
US20080262126A1 (en) * 2007-02-07 2008-10-23 Naturalnano, Inc. Nanocomposite method of manufacture
US20090326133A1 (en) * 2007-05-23 2009-12-31 Naturalnano Research, Inc. Fire and flame retardant polymer composites
US20110086956A1 (en) * 2006-11-27 2011-04-14 Naturalnano, Inc. Nanocomposite master batch composition and method of manufacture
WO2012069577A1 (en) 2010-11-25 2012-05-31 Technip France Flexible submarine pipe comprising a layer comprising a polymer resin comprising aluminosilicate or magnesium silicate nanotubes

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4394253A (en) * 1979-09-26 1983-07-19 Chevron Research Company Hydrocarbons hydroprocessing with imogolite catalyst
US4358400A (en) * 1981-01-12 1982-11-09 Chevron Research Company Residual oil processing catalysts
US4364857A (en) * 1981-01-12 1982-12-21 Chevron Research Company Fibrous clay mixtures
US4499195A (en) * 1982-12-23 1985-02-12 Exxon Research & Engineering Co. Thermally stable mixed oxide gels
US4608357A (en) * 1984-02-06 1986-08-26 Engelhard Corporation Catalytic cracking with mullite composition promoted combustion of carbon monoxide
US4902657A (en) * 1986-06-17 1990-02-20 J. M. Huber Corporation Synthetic alkali metal alumino-silicates, methods and uses, compositions and their methods of preparation
JP5340620B2 (en) * 2008-03-27 2013-11-13 Ｊｘ日鉱日石エネルギー株式会社 Catalyst composition and method for producing aromatic hydrocarbon
US9192912B1 (en) 2011-04-13 2015-11-24 Louisiana Tech University Research Foundation; a Division of Louisiana Tech University Foundation Ceramic nanotube composites with sustained drug release capability for implants, bone repair and regeneration
CN103406120A (en) * 2013-07-19 2013-11-27 常州大学 HNTs/rare earth oxide composite material and its microwave preparation method
CN114599607A (en) * 2019-10-28 2022-06-07 杰富意矿物股份有限公司 Halloysite powder

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2744056A (en) * 1952-09-18 1956-05-01 Gulf Research Development Co Catalytic conversion process employing as catalyst, a halloysite clay activated with magnesium oxide

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2744056A (en) * 1952-09-18 1956-05-01 Gulf Research Development Co Catalytic conversion process employing as catalyst, a halloysite clay activated with magnesium oxide

Non-Patent Citations (5)

* Cited by examiner, † Cited by third party
Title
Barrer et al., "J. Chem. Soc.", 1961, pp. 983-990. *
Barrer et al., "J. Chem. Soc.", 1964, pp. 2296-2305. *
Carroll et al., "Clays and Clay Minerals", 1960, Proceedings of the Seventh Nat. Conf. on Clays & Clay Minerals, pp. 80, 90-99. *
Ross et al., "Halloysite and Allophane", Professional Paper 185-G, 1934, U.S. Dept. of the Interior, pp. 134-144. *
Stubican, "Clays and Clay Minerals", 1960, Proceedings of the Seventh Nat. Conf. on Clays & Clay Minerals, p. 295. *

Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2465775A1 (en) * 1979-09-26 1981-03-27 Chevron Res CATALYTIC PROCESS FOR HYDROGEN TREATMENT OF A HYDROCARBONATED LOAD
US7491263B2 (en) 2004-04-05 2009-02-17 Technology Innovation, Llc Storage assembly
US20050233199A1 (en) * 2004-04-05 2005-10-20 Xingwu Wang Hydrogen storage apparatus comprised of halloysite
US20060163752A1 (en) * 2004-04-05 2006-07-27 Xingwu Wang Storage assembly
US7425232B2 (en) 2004-04-05 2008-09-16 Naturalnano Research, Inc. Hydrogen storage apparatus comprised of halloysite
US20060076354A1 (en) * 2004-10-07 2006-04-13 Lanzafame John F Hydrogen storage apparatus
US20060166810A1 (en) * 2005-01-25 2006-07-27 Gunderman Robert D Ultracapacitors comprised of mineral microtubules
US20060163160A1 (en) * 2005-01-25 2006-07-27 Weiner Michael L Halloysite microtubule processes, structures, and compositions
US7400490B2 (en) 2005-01-25 2008-07-15 Naturalnano Research, Inc. Ultracapacitors comprised of mineral microtubules
US20100171081A1 (en) * 2005-01-25 2010-07-08 Naturalnano Research, Inc. Ultracapacitors comprised of mineral microtubules
US7679883B2 (en) 2005-01-25 2010-03-16 Naturalnano Research, Inc. Ultracapacitors comprised of mineral microtubules
US20070106006A1 (en) * 2005-09-02 2007-05-10 Naturalnano, Inc. Polymeric composite including nanoparticle filler
US7888419B2 (en) 2005-09-02 2011-02-15 Naturalnano, Inc. Polymeric composite including nanoparticle filler
US20110160345A1 (en) * 2005-09-02 2011-06-30 Naturalnano, Inc. Polymeric composite including nanoparticle filler
US8217108B2 (en) 2005-09-02 2012-07-10 Naturalnano, Inc. Polymeric composite including nanoparticle filler
US20110086956A1 (en) * 2006-11-27 2011-04-14 Naturalnano, Inc. Nanocomposite master batch composition and method of manufacture
US8124678B2 (en) 2006-11-27 2012-02-28 Naturalnano, Inc. Nanocomposite master batch composition and method of manufacture
US20080262126A1 (en) * 2007-02-07 2008-10-23 Naturalnano, Inc. Nanocomposite method of manufacture
US8648132B2 (en) 2007-02-07 2014-02-11 Naturalnano, Inc. Nanocomposite method of manufacture
US20080248201A1 (en) * 2007-04-06 2008-10-09 Naturalnano Research, Inc. Polymeric coatings including nanoparticle filler
US20080249221A1 (en) * 2007-04-06 2008-10-09 Naturalnano Research, Inc. Polymeric adhesive including nanoparticle filler
US20090326133A1 (en) * 2007-05-23 2009-12-31 Naturalnano Research, Inc. Fire and flame retardant polymer composites
WO2012069577A1 (en) 2010-11-25 2012-05-31 Technip France Flexible submarine pipe comprising a layer comprising a polymer resin comprising aluminosilicate or magnesium silicate nanotubes
US9664311B2 (en) 2010-11-25 2017-05-30 Technip France Flexible submarine pipe comprising a layer comprising a polymer resin comprising aluminosilicate or magnesium silicate nanotubes

Also Published As

Publication number Publication date
US4098676A (en) 1978-07-04

Similar Documents

Publication Publication Date Title
US4150099A (en) Synthetic halloysites
CA1306735C (en) Stable intercalated clays and preparation method
US3595611A (en) Cation and thermal stabilization of faujasite-type zeolites
US4176090A (en) Pillared interlayered clay materials useful as catalysts and sorbents
US3729429A (en) Layered complex metal silicate compositions and their preparation
US3892655A (en) Layered clay minerals, catalysts, and processes for using
EP0271563A1 (en) Layered silicates and their synthesis.
NZ212014A (en) Preparation of a zeolite and composition thereof
EP0360554B1 (en) Catalysts
US5441630A (en) Hydrodesulfurization process
DE2749024A1 (en) CRYSTALLINE ALUMINOSILICATE ZEOLITHE, THE PROCESS FOR THEIR PRODUCTION AND THEIR USE
JPH0685875B2 (en) Catalyst for catalytic cracking of hydrocarbon oil and catalytic cracking method
CA2016993A1 (en) Synthetic saponite-derivatives, a method for preparing such saponites and their use in catalytic (hydro) conversions
EP0164208A2 (en) Preparation of zeolite beta
US3798177A (en) Novel catalyst support
US3846286A (en) Hydrodesulfurization catalyst
US3686341A (en) Process for aromatization of olefin hydrocarbons
US4217295A (en) Process of catalytic methanation
GB1564004A (en) Manufacture of nickel-containing catalysts and process of catalytic methanation
US3888793A (en) Rare earth chrysotile catalysts
US3692700A (en) Process and compositions for cracking hydrocarbon feeds
DE60108114T2 (en) HYDROTALCIT BASED OXIDES WITH IMPROVED MECHANICAL PROPERTIES
US4018881A (en) High surface area alumina and method for the preparation thereof
EP0018683A1 (en) Process for the preparation of hydrocarbons, and hydrocarbons so prepared
US3630889A (en) Metal nitrides as cracking catalysts